RU2606327C2 - Containers and methods of dispensing doses of liquid concentrate and liquid concentrates of long storage life - Google Patents

Abstract

FIELD: packaging industry.

SUBSTANCE: invention relates to a packaged product having a plurality of doses of liquid concentrate therein, and a method of producing a mixture using batched distribution of liquid concentrate from a vessel using one or more of required properties and features, including almost constant output in a certain range of pressing forces, almost constant output at same pressing force, that is substantially independent of amount of liquid concentrate in vessel, practically not leaking outlet opening, obtaining a jet which ensures minimum spray, when liquid concentrate strikes in a specified liquid, and a jet which maximally facilitates mixing of liquid concentrate with a given liquid to obtain a homogeneous mixture as a whole without using additional devices or agitation. Invention also discloses liquid concentrates of beverages, which can be poured cold in package, and have a shelf life of at least twelve months at normal storage temperatures.

EFFECT: combination of low level of pH and high content of alcohol can be used in concentrate, in particular pH level not higher than 3,5, and alcohol content higher than 5 wt%.

30 cl, 20 dwg, 29 tbl

Description

This application claims the priority of applications: US 61/241,584, filed September 11, 2009, US 61 / 320,155, filed April 1, 2010, US 61 / 320,218, filed April 1, 2010, and US 61 / 374,178, filed August 16, 2010, the full contents of which are hereby incorporated by reference.

FIELD OF TECHNOLOGY

The present application discloses containers and methods for dispensing liquid and, in particular, containers and methods for dispensing doses of liquid concentrate, as well as liquid concentrate for use in such containers or separately from them.

BACKGROUND

Liquid concentrates can be used to reduce the packaging size needed to provide the required amount of the final product. However, liquid concentrates may contain concentrated dyes, so that after mixing the finished product has the desired color. These dyes can stain surfaces, such as clothing, leather, etc., if they get on these surfaces. Thus, a container with concentrated liquid will be unacceptable if, when using such a container, the liquid concentrate will drip or will be supplied from the package in another uncontrolled manner. In some containers, fluid flows from the opening when the user presses the container. When such containers are used to store liquid concentrates, at least two problems arise. Firstly, the above stain problem: if concentrated liquid is supplied from the first vessel to a second vessel in which there is already liquid, then splashing occurs when a stream of concentrated liquid strikes the liquid in the second vessel. This splashing material can stain surrounding surfaces, as well as clothing and skin of the user. In addition, unlike the use of packages, such as a bottle of ketchup or mustard, from which you can squeeze out their contents and visually evaluate the amount of squeezed contents, it is difficult for the user to evaluate how much concentrate has already been dispensed to transfer liquid concentrate from the package to receive necessary final mixture. Another problem may arise when the level of concentrated liquid remaining in the package decreases after several uses. In this situation, the amount of concentrated liquid squeezed out using the same extrusion force can vary significantly with the level of liquid concentrate inside the package.

Liquids, including concentrated liquids, can also be susceptible to spoilage by various microbes, especially if these liquids are placed in containers intended for long-term storage. Known methods for reducing the likelihood of product spoilage and increasing the shelf life of a packaged product include the use in various combinations of heat, pressure, radiation, ultrasound, cooling, natural and artificial antimicrobial and preservative compositions, and the like. Any useful antimicrobial process or antimicrobial composition can act on specific agents that cause spoilage of the product, while their effect on the product itself is minimal. In known methods, preservatives and pasteurization are commonly used in various combinations. Currently, there has been a tendency to reduce the number of preservatives added to food products. Pasteurization complicates and increases the cost of the production process, which is associated with the use of energy to heat the compositions to the pasteurization temperature.

Several attempts to use acidic agents are known, since a low pH provides an antimicrobial effect. However, for many drinks it is difficult to find an acceptable balance between high acidity to provide the desired antimicrobial effect and optimal acidity, which is necessary to ensure the taste of the drink and the stability of the composition. See, for example, US Pat. No. 6,703,056 to Mehansho. Some solutions included balancing the pH level with the alcohol content, as disclosed in JP 2000295976 to Nakamura. This document discloses antimicrobial compositions for acidic drinks containing ethyl alcohol. However, Nakamura compositions also include emulsifiers and propylene glycol. Said beverage compositions are disclosed herein that inhibit crystallization of sucrose fatty acid ester. This document does not disclose compositions with a pH below 3.5, and it does not say anything about concentrates with a long shelf life for acidic drinks.

SUMMARY OF THE INVENTION

The present invention provides containers and methods for dosed dispensing a liquid concentrate using one or more of the necessary properties, including: practically constant delivery in a certain range of pressure forces; almost constant delivery with one pressure force, which does not depend significantly on the amount of liquid concentrate in the tank; an outlet that practically does not spray and does not leak; a stream giving minimal spraying when the liquid concentrate hits a predetermined liquid; and a stream that facilitates mixing the liquid concentrate with the desired liquid to obtain a generally uniform mixture without the use of additional devices or agitation. The container disclosed in this application contains a housing with a pivotally attached lid having an outlet neck attached to it. The container contains an outlet path for the fluid flow, across which a nozzle is located for dispensing from the tank a jet of liquid concentrate having one or more desired properties. The container allows the user to have a relatively small package with liquid concentrate, which can be dispensed repeatedly in small doses into a much larger amount of liquid, such as water, for preparing a beverage.

In one embodiment, the packaged liquid beverage concentrate comprises a container with a lid in which many doses of the liquid beverage concentrate can be placed. In this embodiment, the container with a lid is a housing, a closing lid and a nozzle. The container body has a closed lower end and an upper end having a protrusion that tapers to a neck with an outlet. Between the upper and lower ends, a lateral preferably elastic wall extends, forming the internal volume of the container body, which is accessible through the outlet. The side wall has elasticity, so that it can be squeezed (squeezed) to push the liquid beverage concentrate through the outlet of the neck. In addition, the side wall may further comprise an indicative zone, which is a recess. Such a zone (if used) is preferably located closer to the protrusion than to the lower end of the container body. It provides a tactile indication of the place where the pressure is applied to the side wall to eject the liquid beverage concentrate from the internal volume of the container body and then through the outlet of the neck, which improves the uniformity of the concentrate supply. The lockable lid contains a base that can be attached to the neck of the container body. The base contains a neck with an outlet coinciding with the outlet of the neck of the container body, so that the liquid beverage concentrate leaves the internal volume of the container body through the outlet of the base neck. The lid also contains a closing part, which is attached to the base with a hinge and ensures the closure of the outlet of the neck of the base.

In another embodiment, the packaged liquid beverage concentrate comprises a container with a lid consisting of a container body, a closable lid and a nozzle, and many doses of the liquid beverage concentrate can be placed in the container. The container body has an internal volume for storing there liquid concentrate. The inner volume is formed by a side wall extending between the closed first end and at least partially open the second end. The side wall contains at least one flexible part, which can be deflected by pressure to push the liquid concentrate out of the internal volume of the container body and then through at least partially open second end. The side wall may also have an additional grip area recessed relative to the adjacent parts of the side wall and located closer to the second end than to the first end, to indicate that a compressive force should be applied closer to the second end than to the first end. A lockable lid is attached to the at least partially open second end of the container body and comprises a base and a closing portion attached to the base so that it can be rotated relative to it. The base has an outgoing neck with an outlet. The neck communicates with the internal volume of the container body to form a path for fluid flow between the internal volume of the container and the outlet, so that the pressure pushing the liquid beverage concentrate from the internal volume of the container body pushes it through the outlet of the neck. The nozzle is located in the exhaust tract and has an opening (lumen) designed to form a jet of liquid concentrate having a performance index of the liquid concentrate of less than 4, when the elastic part of the side wall is subjected to a force that creates a mass flow rate of from about 1.0 g / s to about 1.5 g / s

The present invention also provides a method for producing a mixture using a stream of liquid concentrate from a container. The method begins by applying pressure to the flexible part of the side wall of the container, in which many doses of liquid concentrate can be placed for storage. The container also contains an outlet with a nozzle located across the hole. There is a hole in the nozzle (clearance). Then, a stream of liquid concentrate is fed through the nozzle from the tank with a mass flow rate in the range from 1.0 g / s to 3.0 g / s or from 1.0 g / s to 1.5 g / s. After that, a jet is applied to a given liquid inside a given vessel so that when exposed to a noticeable amount of fluid from a given vessel. Then, the predetermined liquid is mixed with the liquid concentrate by means of a jet to obtain a generally homogeneous mixture. The pressure that is required to obtain the desired effluent may depend on the viscosity of the fluid. The viscosity of the liquid concentrate within the vessel may be less than about 75 cP, or less than about 500 cP, and is preferably in the range of about 1 cP to about 25 cP.

The present invention provides compositions of liquid beverage concentrates and methods for their preparation, which can be packaged by cold filling to provide a shelf life of at least twelve months at normal storage temperatures, which compositions are suitable for independent use, or can be used with containers, disclosed in this application. The indicated shelf life can be obtained by combining a low pH and a high alcohol content to ensure the stability of ingredients that are not in themselves stable. Thus, an acidic beverage concentrate can be obtained which has a shelf life at ordinary temperatures of at least twelve months and does not require the use of pasteurization or the addition of preservatives.

In one embodiment, the pH of the concentrate may be less than about 3 or 3.5, and the alcohol content may be at least 1 wt.%. In some embodiments, the compositions and methods for their preparation may contain a cold beverage beverage concentrate that uses a combination of a low pH (lower than about 3) and alcohol (preferably from about 5 wt.% To about 35 wt.%). Various combinations of salts (such as electrolytes) can be added to the concentrate in an amount of from about 0.01 wt.% To about 35 wt.%. Such salts may reduce the activity of water in the compositions to improve antimicrobial activity. The result can be a composition of a liquid beverage concentrate, which: can be stored for at least 12 months; may have a concentration of 75 times or more, preferably up to 100 times, that is, the concentrate is 1/100 of the finished beverage); and may have water activity in the range of from about 0.6 to about 1.0, preferably in the range of from about 0.75 to about 1.0.

The concentrates of the present invention may contain any combination of additives or ingredients, such as water, flavors, nutritional supplements, colorants, sweeteners, salts, buffers, gums, caffeine, stabilizing additives, etc. Additional preservatives, such as sorbate or benzoate, however, they are not necessary to ensure the required shelf life. The concentration of the concentrate can be from about 25 times to about 500 times, from about 75 times to about 160 times, or from about 40 times to about 500 times, and the pH of the concentrate can be from about 1.4 to about 3.0, or 3,5. The pH can be adjusted using food grade acid, such as adipic acid, citric acid, malic acid, fumaric acid, tartaric acid, phosphoric acid, lactic acid, or any other edible organic or inorganic acid. The acid is selected depending on the desired pH level of the concentrate and the desired taste of the diluted product, ready for use. Buffer solutions such as conjugated bases of any acid, such as sodium citrate, potassium citrate, acetates and phosphates, can also be used to adjust the pH of the concentrate. The concentrates may contain a buffer with an acid / buffer weight ratio of about 1: 1 or more, for example, from 1: 1 to 4000: 1, preferably from about 1: 1 to about 40: 1, and more preferably from about 7: 1 to about 15 :one. A drinkable drink may be a diluted concentrate, the volume alcohol content of which may be less than about 0.5%.

Methods for the manufacture of concentrates may include: providing water and additives; providing alcohol in an amount of at least 5 wt.%; adjusting the pH to be less than about 3, and preferably equal to about 2.5 or less. As already indicated, the additives can be flavorings, nutritional supplements, sweeteners, salts, buffers, gums and stabilizing agents. Concentrates can be packaged in a sealed container without the use of pasteurization. A method of manufacturing a concentrate may include: providing a predetermined amount of water; providing potassium citrate; providing a sweetener; providing acids in an amount necessary to obtain a pH level not exceeding about 3; dye supply; providing at least 5 wt.% alcohol; and providing flavoring.

BRIEF DESCRIPTION OF THE DRAWINGS

Figure 1 is a perspective view of a container with a lid in the closed position.

Figure 2 is a schematic perspective view of the container shown in Figure 1, which is pressed to supply a stream of liquid from it to a vessel in which there is a second liquid.

Figure 3 is an enlarged top view in plan of the neck and nozzle of the cap shown in figure 1.

Figure 4 is an enlarged top view in plan of the neck and nozzle of the cap shown in figure 1.

Figure 5 is a perspective view of another version of the container with the lid in the closed position.

Figure 6 is a perspective view of another embodiment of a container with a lid in the closed position.

Figure 7 is a bottom perspective view illustrating the results of tests on the ability of mixing for the tested nozzles (glasses are shown with different levels of the mixture).

Figure 8 is a plan top view illustrating the results of spray tests upon impact of the jet for the nozzle under test (a coffee filter is shown with spray marks on it).

Figure 9 is a plan top view illustrating the results of spray tests upon impact of the jet for the nozzle under test (a coffee filter is shown with spray marks on it).

Figure 10 is a plan top view illustrating the results of spray tests upon impact of the jet for the nozzle under test (a coffee filter is shown with spray marks on it).

Figure 11 is a plan top view illustrating the results of spray tests upon impact of the jet for the nozzle under test (a coffee filter is shown with spray marks on it).

Figure 12 is a plan top view illustrating the results of spray tests upon impact of the jet for the nozzle under test (a coffee filter is shown with spray marks on it).

Figure 13 is a plan top view illustrating the results of spray tests upon impact of the jet for the nozzle under test (a coffee filter is shown with spray marks on it).

Figure 14 is a plan top view illustrating the results of spray tests upon impact of the jet for the nozzle under test (a coffee filter with spray marks on it is shown).

Figure 15 is a graphical representation of the indicator of the ability of mixing and the indicator of spraying upon impact of the jet for the tested nozzles.

Figure 16 is a graphical representation of the difference in mass flow for weak and strong compression for the tested nozzles.

Figure 17 is a graphical representation of the difference in the magnitude of the moment-second for weak and strong pressure for the tested nozzles.

Figure 18 is a graphical representation of the maximum difference between two points of the obtained data for the linearity of flow for the tested nozzles.

Figure 19 is a perspective view of a disassembled container in accordance with another embodiment of the invention.

Figure 20 is a perspective view of the lower part of the lid shown in figure 19.

DETAILED DESCRIPTION OF THE INVENTION

To dispense the liquid concentrate, a container 10 and corresponding methods are proposed in an appropriate manner. Properties of the issuance as necessary include, for example: almost constant issuance in a certain range of pressure forces; almost constant delivery with one pressure force, which does not depend significantly on the amount of liquid concentrate in the tank; an outlet that practically does not spray and does not leak; a stream with minimal spray when the liquid concentrate enters another liquid; and a stream that facilitates mixing the liquid concentrate with another liquid.

Tanks 10 are inherent in some or all of the above properties when dosing a stream of liquid concentrate into a given vessel in which there is a given liquid. The above-described container 10 provides the supply of liquid concentrate in such a way that it flows into a given liquid without significant splashing and spraying, and this creates sufficient turbulence or sufficient mixing inside a given vessel of liquid concentrate and a given liquid to form a generally homogeneous final mixture without the use of additional devices or churning.

Figures 1-6 show options for a container 10 having at least some, and preferably all, of the above properties. The container has a closed first end 12 and at least partially open second end 14, configured to attach the cover 16. The first and second ends 12, 14 are connected by a side wall 18 having a generally tubular shape, which can have any suitable cross section , including a polygonal or curvilinear shape, or combinations thereof, the wall forming the internal volume of the tank. In a preferred embodiment, the container 10 is sized to accommodate many doses (portions) of the liquid concentrate 20. In one embodiment, the dose volume of the liquid concentrate 20 is about 2 cm ³ per 240 cm ^{3 of the} beverage, and the container 10 is designed for about 60 cm ^{3 of} liquid concentrate 20. In another embodiment, the container 10 may contain about 48 cm ^{3 of} liquid concentrate 20.

Variants of the shape of the container 10 are illustrated in figures 1, 3 and 4. As shown in figures 1 and 5, the container 10 has a first end 12, which serves as a base on which can stand 10. The side wall 18 extends generally upward from the base to the second end 14. As already indicated, the cover 16 is attached to the second end 14 by any suitable means, including, for example, a threaded connection with a neck, a snap-fastened connection, adhesive bonding, ultrasonic welding, etc. In a preferred embodiment, the second end 14 includes an upwardly facing protrusion that tapers to form a neck providing a snap-fit connection to the lid 16. In one embodiment shown in FIG. 1, the container 10 may have a generally egg-shaped shape in which the front and rear surfaces 21 bend outward, providing an ergonomic solution to the shape of the container. In another embodiment shown in FIG. 6, the side wall comprises front and rear surfaces 23 that are generally drop-shaped so that the container 10 has an elongated cross section.

In the alternative embodiment shown in FIG. 5, the container 10 may be configured such that it is mounted on a cover 16 attached to the second end 14. In this embodiment, the cover 16 has a generally flat upper surface so that the container 10 can stand stably on the cover 16. In addition, since the first end 12 should not in this case serve as the basis for the container 10, the side wall 18 may taper as it moves from the second end 14 to the first end 12 to form a narrow first end 12, as it is shown about in figure 5. The side wall 18 may also include a recessed part 25, which can mate with the side wall 18 in a front view and have an inverted drop-shaped shape, as shown in figure 5. In addition, as shown in figures 5 and 6, the side wall 18 may also have a recess 22 serving as a grip area. In one embodiment, the recess 22 is horizontally centered on the side surface 18 of the container 10. Preferably, the recess 22 is located closer to the second end 14 of the container 10. This arrangement of the recess 22 is preferable because as the liquid concentrate 20 is consumed from the container 10, there is free space filled with air. The liquid concentrate 20 is supplied more evenly if the pressure is applied to those places in the container 10 in which there is a liquid concentrate 20, and not in those places where the air bubble is. When supplying the liquid concentrate 20, the container 10 is turned over so that the second end 14 with the cover 16 is lower than the first end 12, so that during the metered supply of the liquid concentrate, the first end 12 contains the air in the container 10. In this embodiment, the recess 22 can serve as a pointer for a user's finger squeezing the liquid concentrate 20 from the container 10. As shown in the figures, the recess 22 may have a generally round shape, but other shapes, such as polygonal, curved, or combinations thereof are possible.

Figures 1-6 illustrate various options for the cover 16. In these embodiments, the cover 16 is a hinged upper part with a base 24 and a covering part 26. An opening is formed in the lower part of the base 24, which is connected to the second end 14 of the container 10 and communicates with the internal volume containers 10. The upper surface 28 of the base 24 contains a neck 30, forming an outlet opening 31, which opens outward. The neck 30 continues the opening formed in the lower part of the base 24 to provide an outlet or exhaust path for the flow of liquid concentrate 20 present inside the tank 10.

In one aspect, the neck 30 comprises a nozzle 32 located inside it, located across the outlet path, which restricts the flow of fluid from the reservoir 10 to form a jet 34 of liquid concentrate 20. FIGS. 3 and 4 illustrate embodiments of the nozzle 32 for use in the reservoir 10. As shown in FIG. 3, the nozzle 32 is a generally flat plate 36 having a through hole, a through channel or passage 38. The through channel 38 may have straight edges or tapering walls. In the alternative embodiment shown in figure 4, the nozzle 32 is a generally flat flexible plate 40, which may be made of silicone or similar material and in which there are slots 42, preferably two intersecting slots 42, forming four wings 44 having whole triangular shape. With such a device, when the container 10 is squeezed, for example, by pressing the side wall at the recess 22, the liquid concentrate 20 is pushed to the nozzle 32, the leaves 44 of which extend outward, allowing the flow of the liquid concentrate 20. The stream 34 of the liquid concentrate formed by the nozzle 32 , strikes with a force determined by the speed and mass flow rate of the jet into a given liquid 43 in a given vessel 45 to create turbulence in a given liquid 43 and form an almost uniformly mixed final product without using tions any adaptations or shaking.

The cover portion 26 of the cover 16 is generally dome-shaped and is designed to interface with the neck 30 extending from the base 24. As shown in FIG. 2, the cover portion 26 is connected to the base 24 using a hinge 46. The cover portion 26 may also comprise a plug portion ( plug) 48, extending from the inner surface 50 of the cover of the lid. Preferably, the closure portion 48 is sized and shaped so that it fits snugly into the neck 30 to provide additional protection against accidental release of the liquid concentrate 20 or other leakage. In addition, in one embodiment, the closure portion 26 may be latched onto the base 24 to block access to the interior 19 of the container 10. In this case, a recessed portion 52 adjacent to the closure portion 26 may be formed on the base 52 when it is turned to the closed position. The recessed portion 52 may provide access to the edge 54 of the cover portion 26, so that the user can click on the edge 54 to open the cover portion 26.

In an alternative embodiment, the container 110 is similar to the container 10 shown in figures 1-6, but it contains a modified cover 116 and a modified second end 114 of the container 110, as shown in figures 19 and 20. Similarly to the previous embodiment, the cover according to such an alternative embodiment of the container is the top a cap with a closing part 126 and a base 124. An opening is formed in the lower part of the base 124, which is connected to the second end 114 of the container 110 and communicates with the internal volume of the container 110. The upper surface 128 of the base with erzhit neck 130 forming outlet opening 131 that opens outward. The neck 130 continues the opening formed in the lower part of the base 124 to provide an outlet or exhaust path for the flow of liquid concentrate 20 present inside the tank 110. The neck 130 comprises an nozzle 132 located inside it located across the exhaust path, which restricts the flow of fluid from the tank 110 to form a jet of liquid concentrate. The nozzle 132 may be one of the nozzles shown in figures 3 and 4 and discussed in the present description.

As in the previous embodiment, the cover portion 126 of the cover 116 is generally dome-shaped and adapted to mate with the neck 130 extending from the base 124. The cover portion 126 may also include a plug portion 148 extending from the inner surface 150 of the cover portion. Preferably, the plug portion 148 is sized and shaped so that it fits snugly into the neck 130 to provide additional protection against accidental release of the liquid concentrate or other leakage. The closure portion 148 may be a hollow cylindrical protrusion, shown in figures 19 and 20. Inside the closure portion 148 may be located additionally protruding from it an inner tube 149. This tube 149 can interact with the flexible plate 40 of the nozzle 32 to limit the movement of the plate 40 from the concave position in which the flaps are closed, in a convex position in which the flaps are at least partially open to discharge liquid concentrate. The inner plug 149 further prevents leakage or leakage of fluid from the container 110. The plug portion 148 and / or plug 149 interact with the nozzle 132 and / or the neck 130 to at least partially block the fluid flow.

The closure portion 148 may be shaped and sized such that when it closes the neck 130, the user will hear and / or feel one, two or more clicks with his hand. For example, sliding the back portion of the clogging portion 148 over the back of the neck 130 (closer to the hinge) may cause an audible or tangible click as the cover portion 126 moves toward the closed position. Further movement of the closure portion 126 toward its closed position may cause a second audible and tangible click, as the front portion of the closure portion slides along the front of the neck 130 (on the opposite side of the hinge). In a preferred embodiment, a second audible and tangible click occurs immediately after the closure of the closing part 126. The sound and / or tactile feedback signals of the closure of the closure part 126 can be provided.

The closure portion 126 can be snapped onto the base 124 to block access to the interior of the container 110. In this case, a recessed portion 152 can be formed on the base 124 adjacent to the closure portion 126 when it is rotated to the closed position. The recessed portion 152 can then provide access to the edge 154 of the cover portion 126, so that the user can click on the edge 154 to open the cover portion 126.

To attach the cover 116 to the neck 114 of the container 110, it is provided with an annular inclined protrusion 115 extending in the radial direction. The skirt 117 extending from the bottom surface of the base 124 of the cover 116 has an inwardly extending edge 119. This edge 119 is located on the skirt 117 so that it can slide along the protrusion 115 and then occupy a position behind this protrusion to attach the cap 116 to the neck 114. In a preferred embodiment, the inclined protrusion 115 is designed so that a smaller force is required to attach the cover 116 compared to the force required to remove it. To limit the rotation of the lid 116 after it is mounted on the container 110, one or more outgoing longitudinal protrusions 121 are formed on the neck 114. Each such protrusion 121 is included in a notch 123 formed in the skirt 117 of the lid 116. The interaction between the lateral edges of the protrusion 121 and the lateral edges of the notch 123 restricts the rotation of the lid 116 and holds it in a preferred position, especially when the parts of the lid 116 should be flush with the side wall 118 of the container 110. In the embodiment shown in figures 19 and 20, two heights are used upa 121 and two notches 123 which are spaced apart circumferentially by 180 degrees.

The containers disclosed herein can have elastic side walls that can be squeezed to dispense a liquid concentrate or other contents from the container. By elasticity is meant the property of the walls to fully or at least as a whole return to their original shape when the compression is stopped. The containers can be equipped with structural elements that limit the displacement of the side wall, that is, the degree of compression of the side walls. This may contribute to uniformly discharging contents from the container. For example, the aforementioned recess may act as a limiter when it can abut against the opposite side of the side wall to limit further compression of the opposite parts of the side wall. The depth and / or thickness of the recess may vary to provide the desired degree of restriction. Other protrusions on one or both side walls (such as opposite recesses or protrusions) can be used as such stops.

The container options and their advantages disclosed in the present description are illustrated by the examples below, however, the specific conditions, technological schemes, materials and their quantities indicated in these examples, as well as other conditions and specific details, should not be construed as limitations of the method and device.

EXAMPLES

Tests were carried out on various nozzles used as an outlet in a container made of high density polyethylene and ethylene-vinyl alcohol and containing approximately 60 cm ^{3 of} liquid. Table 1 below shows the injectors tested and their abbreviations.

Table 1 test nozzles Name Abbreviation SLA, straight edge, 0.015 inches O_015 SLA, straight edge, 0.020 inches O_020 SLA, straight edge, 0.025 inches O_025 LMS V21 Engine, 0.070 inches crosswise V21_070 LMS V21 Engine, 0.100 inches, crosswise V21_100 LMS V21 Engine, 0.145 inches, crosswise V21_145 LMS V21 Engine, 0.200 inches, crosswise V21_200

SLA nozzles, straight edge, have a front plate with a through circular hole having straight edges; manufacturing method - stereolithography. The number after the hole identifier indicates its approximate diameter. The LMS designation refers to a silicone valve located in a nozzle having a cross-shaped slot, manufactured by Liquid Molding Systems, Inc. (LMS), Midland, Michigan. The flaps of the cruciform nozzle flexibly bend to let the product out of the container and at least partially return to their original position to prevent unwanted fluid from flowing through the valve. This prevents leakage of liquid from the tank, which, as already indicated, is important for liquid concentrates. The number after the identifier indicates the length of each cruciform segment. It is assumed that when used together with the containers disclosed in the present description, the valve allows outside air to pass into the container at the cleaning stage when the pressure on the walls of the container is stopped to clean the valve and parts of the exhaust path passing through the container and / or cover. In addition, it is contemplated that such a combination provides controlled outflow of concentrate when the valve is directed downward, so that air that has entered in during the purification step is removed from the exhaust path. Another suitable valve is the LMS V25 Engine, 0.070 inches, a cross-shaped slot.

An important feature of the nozzle is its ability to mix the ejected liquid concentrate with a given liquid, usually water, using only the force created by the stream of liquid concentrate striking the water. An acidity level (pH) can be used to evaluate the degree of mixing of the two liquids. For example, a liquid concentrate poured from a cup leaves distinct dark and light streaks. However, a stream of liquid concentrate can reach the bottom of a given vessel and then swirl back to the surface of a given liquid, as a result of which the color difference of the strips is significantly reduced. To determine the composition of the mixture, the pH level can be measured in real time. Tests included the release of 4 cm ^{3 of} liquid concentrate in 500 ml of water at room temperature 25 ° C. The liquid concentrate was poured from a small cup, and the stream was obtained using a 6 cm ³ syringe with an outlet of approximately 0.050 inches. Mixing (last row of Table 2) until a homogeneous mixture was carried out using a Magnastir mixer.

table 2 mixing pH values Flow from the cup Syringe jet Attempt 1 Attempt 2 Slow (1.5 s) Avg (1 s) Fast. (0.5 s) Time At the bottom Up At the bottom Up At the bottom Up At the bottom Up At the bottom Up 0 5.42 5.34 5.40 5.64 5.50 5.54 5.54 5.48 5.56 5.59 5 3.57 4.90 3.52 5.00 3.19 4.10 3.30 3.70 2.81 2.90 10 3.37 4.70 3.33 4.80 2.97 3.20 3.25 3.45 2.78 2.80 fifteen 3.33 4.70 3.22 4.70 3.00 3.10 3.27 3.40 2.77 2.78 twenty 3.32 4.60 3.16 4.70 3.01 3.10 3.13 3.30 2.75 2.80 25 3.31 4.60 3.12 4.70 3.01 3.08 3.08 3.20 2.74 2.80 thirty 3.31 4,50 3.10 4.70 3.01 3.07 3.06 3.18 2.73 2.75 35 3.30 4.30 3.09 4.70 3.00 3.06 3.05 3.17 2.72 2.75 40 3.28 4.25 3.10 4.70 3.00 3.07 3.06 3.17 2.71 2.70 Mixture 2.78 2.70 2.67 2.70 2.65

40 seconds after pouring the concentrate from the cup, the pH was 3.28 at the bottom and 4.25 at the top in the first attempt and 3.10 at the bottom and 4.70 at the bottom in the second attempt.

Tests for the jet were carried out at low, medium and high feed rates. After 40 seconds, the pH level was 3.07 at the bottom and 3.17 at the top at low speed, 3.06 at the bottom and 3.17 at the top at medium speed and 2.71 at the bottom and 2.70 at the top at high speed. The above results show the effectiveness of using a jet of liquid concentrate to mix it with a given liquid. Therefore, to obtain a mixture with a difference in pH levels in the upper and lower parts of the vessel of about 0.3, a stream of liquid concentrate can be effectively used. In fact, this result was obtained after 10

second after the start of the jet.

Tests of each of the above nozzles were carried out to determine the indicator of mixing ability. The mixing ability indicator is a value that is visually evaluated on a scale of 1-4, where 1 is excellent, 2 is good, 3 is satisfactory, 4 is bad. The “poor” rating corresponds to the situation when the liquid layers are not mixed, that is, the water layer is on the liquid concentrate layer (the nozzle has no effect). A satisfactory rating corresponds to a situation with a low degree of mixing of the liquid concentrate with water, and the layers of the liquid concentrate and water are clearly distinguished (the nozzle for some reason does not work well). The “good” rating corresponds to the situation when the necessary mixing occurred in more than half of the vessel, and at the same time there are small layers of water and liquid concentrate on each side of the mixed liquid. The rating “excellent” corresponds to the situation when the required effective mixing occurred without noticeable separation of the layers of liquid concentrate and water.

In the tests, 4 cm ^{3 of} liquid concentrate, which was 125 g of citric acid in 500 g of water, with 5% SN 949603 (flavor) and 1.09 g / cm ^{3 of} Blue # 2 dye, were introduced into a 250 ml glass beaker containing 240 ml of water. The viscosity of the liquid concentrate was approximately 4 cP. Table 3A presents the results of the mixing tests (a measure of the mixing ability for each nozzle).

Table 3A indicator of mixing ability for each nozzle Nozzle Mixability Index 0015 3 0020 2 0025 one

V21_070 one V21_100 one V21_145 2 V21_200 2

Figure 7 shows the results of mixing a liquid concentrate and water for each nozzle tested. Dotted lines have been added to the images of the glass with the liquid to indicate approximate boundaries between clearly visible layers. The above Table 3A and the images in figure 7 show that the hole with straight edges with a diameter of 0.025 inches, a cross-section of a size of 0.070 inches and a cross-section of a size of 0.100 inches provide mixed liquids with an excellent indicator of mixing ability (homogeneous mixture in a glass with almost uniform color throughout volume). A bore with straight edges of 0.020 inches in diameter, a cross-section of 0.145 inches and a cross-section of 0.200 inches provide mixed liquids with a good indicator of mixing ability (after applying 4 cm ^{3 of} liquid concentrate, small layers of water and liquid concentrate are visible). A straight-hole with a diameter of 0.015 inches provided a mixed liquid, the mixing ability of which could be rated as “good”, but in this case it was rated “satisfactory” due to the long delivery time of 4 cm ^{3 of} liquid concentrate, which should be considered as unacceptable inconvenience to a potential user.

In other tests, the indicator of mixing ability was determined depending on the pressure created by the air supplied to the tank for different valve configurations. More specifically, the tests were conducted for simulated pressure forces with gradations of "low pressure", "medium pressure" and "strong pressure". The air supplied under pressure to the tank simulated the pressure force (although in reality in the tests pressure on the side walls was not carried out). At the beginning of each test, the required air pressure was set using the regulator. Air from the outlet of the pressure regulator was supplied through a tube to a sealed unit connected to the inlet in the center of the lower part of the tank. The capacity can be oriented at an angle of about 0-10 degrees relative to the vertical. After the air pressure regulator, a push button was installed that connects with a 2-foot, 5/32 inch pipe to a sealed connector. For each test, the container was filled with contents to its preferred maximum volume (may be less than the total volume of the container). Pressed the button for the estimated time, ensuring the issuance of a given dose. The nozzle of the container was at a height of 2-4 inches from the surface of a given liquid. The same technique was used to determine other parameters related to simulated pressure. The results are consistent with the results obtained in tests with real pressure, and show that the larger the size of the nozzles with a cross-shaped cross-section, the more spray occurs. In simulated pressure tests, the time required to dispense 4 cm of liquid concentrate from a container containing about 49 cm ^{3 of} concentrate in a total volume of 65 cm ^{3 was} recorded. The container had a shape similar to that shown in FIG. 6 and contained a screw cap 24-410 with a nozzle, a wall about 0.03 inches thick in high density polyethylene, the distance from the bottom of the tank to the valve being about 3 inches, and the thickness of the tank was approximately 1.1 inches, the maximum width was approximately 2.25 inches, and the neck diameter was approximately 1 inch. The density of the concentrate was approximately 1.1 g / cm ³ , the viscosity was 4 cP, and the color of the concentrate was sufficient to indicate the color of the final beverage. Simulated pressure test results are presented in Table 3B.

Table 3B indicator of mixing ability for each nozzle (simulated pressure) Nozzle Light touch (40) (inches VST) Medium Press (60) (inches w.st.) Strong Press (100) (inches w.st.) The average mixing ability O_015 one 2 2 1,67 O_020 2 2 1,67 O_025 2 one 1.33 V21_070 3 2 2.00 V21_100 2 one 1.33 V21_145 3 one 1,67

V21_200 I one 1.00

As already indicated, another important characteristic of the nozzle used for the dosed supply of liquid concentrate is the degree of spraying or splashing that occurs when a stream of liquid concentrate falls into a vessel with liquid. Concentrated dyes of liquid concentrate can stain surrounding surfaces, as well as clothing and skin of the user. In this regard, each nozzle was tested to determine the impact spray ratio. Tests to determine the impact spray ratio were carried out using a 400 ml beaker filled with water tinted with blue dye to a level of 1 inch from the bead edge. Then, using a rubber band on the glass, a round coffee filter was fixed so that the flat surface of the filter was about 1 inch above the edge of the glass. Since the upper surface of the filter was 1 inch above the edge of the beaker, the filter has a side wall on which traces of liquid spilling on the sides remained, which is undesirable due to the appearance of dirty spots. A cut-out was made in the coffee filter, extending slightly onto the upper surface, to supply liquid concentrate to the vessel. Then, a bottle with nozzles attached to it was held above the edge of the glass, and five times the liquid was fed from it in the center of the glass. After that, the filter was removed and the impact spray ratio for each nozzle was determined from it. The impact spray ratio is a value visually evaluated on a scale of 1-4, where 1 is excellent, 2 is good, 3 is satisfactory, 4 is bad. The rating “excellent” corresponds to the situation when there are no splashes in the central zone of the filter located above the glass, or there are small splashes, and outside the central zone (peripheral zone) the amount of splashes is minimal, or there are none at all. A rating of “good” corresponds to a situation where there are splashes in the central zone and small splashes in the peripheral zone. A rating of “satisfactory” corresponds to a situation where there are splashes in the central zone and medium-sized splashes in the peripheral zone. A rating of “poor” corresponds to a situation where there are splashes in the central zone and large splashes in the peripheral zone.

Table 4A impact spray indicator for each nozzle Nozzle Impact Spatter O_015 one

O_020 one O_025 2 V21_070 one V21_100 3 V21_145 3 V21_200 four

In figures 8-14 and Table 4A presents the results of determining the indicator of impact spray for each test nozzle. Nozzles with a diameter of 0.015 and 0.020 inches with straight edges of the holes, as well as a nozzle with a cross-shaped cross section of 0.070 inches, received a rating of "excellent" for the impact spray ratio, since the spray created by the liquid stream did not lead to significant spray marks on the coffee filter, as this is shown in figures 8, 9 and 11, respectively. A nozzle with a diameter of 0.025 inches with straight edges of the hole caused small marks of spray on the side wall of the coffee filter, as shown in figure 10, so she was rated "2" by the indicator of impact spray. Crosswise nozzles of 0.100 and 0.145 inch sizes caused large spray marks on the side of the filter, as shown in FIGS. 12 and 13, and accordingly received a “3” impact spray rating. Finally, a 0.200-inch cross-shaped nozzle caused significant spray marks on the side of the filter, indicating a large amount of liquid was spilled from the cup. In this regard, the nozzle with a cross-sectional size of 0.200 inches received a rating of "4" impact spray.

Similar tests were also carried out to determine the impact spray ratio, but with an adjustable pressure parameter on the walls ("weak pressure", "medium pressure", "strong pressure"), and the degree of pressure was simulated by the pressure of the air supplied to the container. At the beginning of each test, the required air pressure was set using the regulator. Air from the outlet of the pressure regulator was supplied through a tube to a sealed unit connected to the inlet in the center of the lower part of the tank. The capacity can be oriented at an angle of about 0-10 degrees relative to the vertical. After the air pressure regulator, a push button was installed, which was connected by a 2-foot 5/32 inch pipe to a sealed connection unit. For each test, the container was filled with contents to its preferred maximum volume (may be less than the total volume of the container). Clicked on the button for the estimated time, ensuring the supply of a given dose. The nozzle of the container was at a height of 2-4 inches from the surface of a given liquid. The tests were carried out with simulated pressure on the side walls of the tank. The results are consistent with the results obtained in tests with real pressure, and show that the larger the size of the nozzles with a cross-shaped cross-section, the more there is a spray. In simulated pressure tests, the time required to dispense 4 cm ^{3 of} liquid concentrate from a container containing approximately 49 cm ^{3 of} concentrate in a total volume of 65 cm ^{3 was} recorded. The container had a shape similar to that shown in FIG. 6 and contained a wall about 0.03 inches thick in high density polyethylene, the distance from the bottom of the tank to the valve being about 3 inches, the thickness of the tank being about 1.1 inches, and the maximum width was approximately 2.25 inches and the neck diameter was approximately 1 inch. The density of the concentrate was approximately 1.1 g / cm3, the viscosity was 4 cP, and the color of the concentrate was sufficient to indicate the color of the final beverage.

Table 4B impact spray indicator for each nozzle (simulated pressure) Nozzle Light touch (40) (inches VST) Medium Press (60) (inches w.st.) Strong Press (100) (inches w.st.) Average impact spatter O_015 one one one 1.00 O_020 one one one 1.00 O_025 one one one 1.00 V21_070 one one one 1.00 V21_100 one one one 1.00 V21_145 3 one 2 2.00 V21_200 3 four 2 3.00

The figure 15 presents the indicators of the ability of mixing and impact spray obtained for each nozzle in tests using real pressure on the side walls of the tank. These test results can be combined, for example folded, to form an indicator of the performance of the liquid concentrate for each nozzle. As a result of the tests, it was found that the nozzle with a crosswise cross section of 0.070 inches in size provides an indicator of the performance of the concentrate equal to 2, since it provides excellent mixing of the concentrate with the liquid, and also its operation is characterized by minimal spraying. For nozzles with a diameter of 0.020 and 0.025 inches with straight edges of the holes, estimates of "3" were obtained, that is, they provide a sufficiently good final product. A nozzle with a diameter of 0.015 inches with straight edges of the hole and a nozzle with a cross-shaped cross-section of 0.100 inches received a rating of "4", and nozzles with a cross-shaped cross-section of 0.145 and 0.200 inches received a rating of "5" and "6", respectively. Considering the results obtained, it can be said that the performance indicator of the liquid concentrate for the nozzle used with the container disclosed in this application should be in the range of 1-4 so that a good product can be obtained, and preferably in the range of 2-3.

Then, for each nozzle, the average jet velocity was calculated for weak and strong pressure. A horizontal water bottle was installed horizontally for each nozzle at a height of 7 inches from the surface. Then a predetermined force was applied, and the distance to the center of the obtained water mark (within 0.25 feet) was measured. Air resistance was not taken into account. The indicated actions were performed three times for each nozzle using both pressure forces. The average values are shown in Table 5.

Table 5 average speed calculated for each nozzle using weak and strong pressures Nozzle Speed (mm / s) (weak) Speed (mm / s) (strong) O_015 5734 7867 O_020 6000 8134 O_025 6400 7467 V21_070 6400 7467 V21_100 5600 8134

V21_145 4934 6134 V21_200 4000 5334

Then, tests were conducted for each nozzle to determine the amount of fluid (g / s) passing through the nozzle, for both weak and strong pressure). The exposure was carried out for 3 seconds, and then the ejected liquid was weighed. To determine the flow rate, the obtained value had to be divided into three. The results obtained are presented in Table 6.

Table 6 mass flow for low and high pressures for each nozzle Nozzle Mass flow (g / s) (low pressure) Mass flow (g / s) (high pressure) O_015 0.66 0.83 O_020 1.24 1.44 O_025 1.38 1.78 V21_070 1.39 2.11 V21_100 2.47 3.75 V21_145 2,36 4.16 V21_200 2.49 4.70

The graph shown in figure 16, shows the difference in mass flow for weak and strong pressures for each nozzle. A relatively small difference in the mass flow rate of the liquid concentrate is desirable, since this means that the user will squeeze out almost the same amount of concentrate, even if different pressure forces are used. In this case, almost the same amount of the mixture is supplied, which, in relation to the prepared beverage, directly affects its taste, for the same extrusion time with different efforts. As can be seen in figure 16, the nozzles with a cross-section of 0.100, 0.145 and 0.200 inches in size provide a much higher concentrate flow rate and also have a higher difference for weak and strong pressures, that is, in these cases, maintaining a constant pressure force is more important when issuing a concentrate to obtain homogeneous mixtures.

Then the mass flow rate for each nozzle can be used to calculate the time it takes to dispense 1 cm ^{3 of} liquid. The tests were carried out with water, for which 1 g is equivalent to 1 cm ³ . Accordingly, by dividing 1 by the above mass flow rates, it is possible to obtain the time required to dispense 1 cm ^{3 of} liquid through each nozzle. These values are shown in Table 7A.

Table 7A dispensing time of 1 cm ³ liquid for weak and strong pressure for each nozzle Nozzle Dispensing time 1 cm ³ (sec) (slight pressure) Dispensing time 1 cm ³ (sec) (strong pressure) O_015 1,52 1.20 O_020 0.81 0.69 O_025 0.72 0.56 V21_070 0.72 0.47 V21_100 0.40 0.27 V21_145 0.42 0.24 V21_200 0.40 0.21

Convenience tests have shown that the acceptable range of times for dispensing a dose of liquid concentrate is 0.3-3.0 seconds, which includes dispensing times at which the user can control the process of squeezing out the liquid concentrate, or which he could allow to obtain a reasonably specified amount liquid concentrate. A range of from about 0.5 sec / cm ³ to about 0.8 sec / cm ³ provides sufficient time in terms of user response for a standard dose of about 2 cm ³ per 240 ml or about 4 cm ³ per standard bottle of water, and however, the time will also not be burdensome for the consumer, since it will not require too much time to issue a standard dose. Nozzles with a diameter of 0.020 and 0.025 inches with straight edges of the holes, as well as a nozzle with a cross-sectional size of 0.070 inches provide the indicated values regardless of the pressure force (weak or strong). Tests and calculations to determine the flow characteristics of the concentrate were carried out with a compressed air supply, the pressure of which corresponded to weak, medium and strong pressures, to calculate the time required to dispense 4 cm ³ of the beverage concentrate from a container containing approximately 49 cm ³ concentrate in a total volume of 65 cm First, the mass flow rate was determined by placing the inverted container at a height of about 6 inches above the drainage tray located on the Instron weight sensor. Then, the aforementioned pressure providing system simulated a weak, medium and strong pressure force. Instron sensor output was analyzed to determine mass flow. Then, the obtained mass flow rate can be used to calculate the time required to dispense a given amount of concentrate, for example, 2 cm ³ , 4 cm ³ etc.

Typically, the time for delivering the dose of the concentrate should not be too long (since this can increase the spread in time and, accordingly, in the amount of the concentrate supplied) or too short (since this can lead to the inability to control the amount of concentrate dispensed within a reasonable range). The time (duration) of the delivery of liquid concentrate can be measured on a scale of 1 to 4, where 1 corresponds to an easily controlled quantity or dose, that is, the delivery time is sufficient to provide some control without too much change (for example, on average in the range of 1-3 sec for 4 cm ³ ); 2 corresponds to a dose that is given for a slightly longer or shorter time, but the dose can still be controlled (for example, on average in the range of 0.3-1 sec or in the range of 3-4 sec for 4 cm ³ ) ; 3 corresponds to a dose that is difficult to control, because the time is too short or too long, and this provides either minimal or too large a possibility of regulation (for example, on average about 0.3 sec (and some points may be less than 0.3 sec) or in the range of 4-10 seconds for 4 cm); and 4 corresponds to the dose, which is even more difficult to adjust for the same reasons that are indicated for the assessment of "3" (on average less than 0.3 sec (all points less than 0.3 sec) or more than 10 sec for 4 cm ³ ) Then determined Estimation of the delivery time for the average pressure force, determined by the weak, medium and strong simulated pressure. The results obtained are presented in Table 7B.

Table 7B Dosed dispense time of 4 cm ³ of beverage concentrate (simulated pressure) Nozzle Light touch (40) (inches VST) Medium Press (60) (inches w.st.) Strong Press (100) (inches w.st.) Average time Rating O_015 13.3 13.3 6.7 11.1 four O_020 4.0 3.3 2.9 3.4 2 O_025 2, S 2.5 2.0 2,3 one V21_070 3.3 2.0 1.3 2.2 one V21_100 0.5 0.4 , 2 0.3 2 V21_145 0.3 <0.3 <0.3 0.3 3 V21_200 <0.3 <0.3 <0.3 <0.3 four

The mixing ability metric, impact spray metric, and dispensing time estimate (whether the pressure is real or simulated) can be multiplied to determine the functional metric for dispensing liquid concentrate (LCDFV). Low LCDFV is preferred. For example, preferred LCDFV values are in the range of 1-4. Examples of LCDFV metrics for the above metrics (metric of mixing ability, metric of impact spatter, and estimated dispensing time) for simulated pressure are shown in Table 7C. As you can see, valve V21_070 and nozzle O_025 have the lowest values of LCDFV. Although the nozzle O_025 has a lower LCDFV value compared to the valve V21_070, the nozzle has very poor performance according to the results of the spray test.

Table 7C LCDFV value for each nozzle Nozzle LCDFV O_015 6.7 O_020 3.3 O_025 1.3 V21_070 2.0

V21_100 2.7 V21_145 10.0 V21_200 12.0

The area of the holes of each of the nozzles is shown in Table 8.

Table 8 nozzle hole area for low and high pressure Nozzle Hole area (mm ² ) (slight pressure) Hole area (mm ² ) (strong pressure) O, 015 0.114 0.114 O_020 0,203 0,203 O_025 0.317 0.317 V21_070 0.217 0.283 V21_100 0.442 0.461 V21_145 0.479 0.678 V21_200 0.622 0.881

The area of the round holes of the SLA nozzles was determined by the formula πr ² . The areas of the cruciform slots were calculated by multiplying the calculated amount of material discharged by a thousand and dividing by the calculated speed, both for weak and strong pressures.

Finally, a moment-second value was calculated for each nozzle using weak and strong pressures. This value is calculated by multiplying the calculated mass flow rate by the calculated speed. The results are shown in Table 9A.

Table 9A moment-second value of each nozzle for weak and strong pressures (actual pressures) Nozzle Moment second (slight pressure) Moment-second (strong pressure) O_015 3803 6556 O_020 7420 11686 O_025 8854 15457 V21_070 8875 15781

V21_100 13852 30502 V21_145 11660 25496 V21_200 9961 25068

The moment-second value for each nozzle was also determined using the method described above to form weak, medium, and strong simulated pressures using compressed air. The mass flow rate (indicated in Table 9B) was multiplied by the speed (indicated in Table 9C) to obtain the moment-second value for simulated pressures (indicated in Table 9D).

Table 9B mass flow rate (g / s) of each nozzle for simulated pressure Nozzle Light touch (40) (inches VST) Medium Press (60) (inches w.st.) Strong Press (100) (inches w.st.) Average mass flow (g / s) O_015 0.3 0.3 0.6 0.4 O_020 1,0 1,2 1.4 1,2 O_025 1.6 1,6 2.0 1.7 V21_070 1.2 2.0 3.0 2.1 V21_100 8.0 11.3 25 14.8 V21_145 14.0 X X X V21_200 X X X X

Table 9C initial speed (mm / s) for each nozzle (simulated pressure) Nozzle Light touch (40) (inches VST) Medium Press (60) (inches w.st.) Strong Press (100) (inches w.st.) Average initial speed (mm / s) 0015 2400 4000 5600 4000 0020 4000 5600 7200 5600 0025 4000 4800 6000 4934 V21070 4400 5200 7600 5734

V21_100 4400 4800 6400 5200 V21_145 4000 4800 6400 5067 V21_200 4000 4800 5600 4800

Table 9D moment-second value for each nozzle for weak, medium and strong pressure (simulated pressure) Nozzle Light touch (40) (inches VST) Medium Press (60) (inches w.st.) Strong Press (100) (inches w.st.) Average moment-second O_015 720 1200 3360 1760 O_020 4000 6720 10081 6934 O_025 6400 7680 12001 8694 V21_070 5280 10401 22801 12827 V21_100 35202 54403 160010 83205 V21_145 56003 X X X V21_200 X X X X

The moment-second values are related to the ability to mix a jet of liquid leaving the nozzle, since it depends on the mass flow rate and speed, that is, on the quantity and speed of the liquid supplied from the tank. However, tests have shown that the consumer will squeeze approximately the same amount of liquid concentrate, even if it applies different pressure forces. Thus, an almost homogeneous mixture will be provided for equal values of the feed time with different pressure forces. The results obtained for real and simulated pressures are in good agreement. As already shown, simulating the operation of the opening with the valve can provide more comparable moment-second values for weak and strong pressures, as well as for the range of simulated pressures, and at the same time, the valve prevents the concentrate from leaking out.

The graph shown in figure 17, shows the difference in the values of the moment-second for weak and strong pressures for each nozzle. For a liquid concentrate, it is desirable to have a relatively small moment-second difference, since the zero difference corresponds to a constant moment-second value that is independent of the pressure force. Changes in the moment-second magnitude, not exceeding about 10,000 and preferably 8,000, will be relatively small for weak and strong pressures, so that the jet leaving the tank and falling into a given liquid will in this case have approximately the same energy, which ensures almost the same mixtures. As shown in figure 17, nozzles with a round hole and a nozzle with a cross-shaped slot of size 0.070 inches give such a difference in the values of the moment-second, which provides completely comparable mixtures for weak and strong pressure. Also acceptable moment-second differences may be about 17,000 or less, or about 12,000 or less.

Another important characteristic is the ability of a container for liquid concentrate to dispense it in doses almost linearly over a wide range of quantities of liquid concentrate in the container when a constant pressure is applied for a given time. Nozzles were tested to determine the weight of the liquid concentrate pushed out under pressure, which provides the minimum controlled speed for a given time interval when the tank is filled with liquid concentrate to low, medium and high levels. The results of these tests are shown in Table 10.

Table 10 amount of concentrate dispensed depending on the level of filling the tank with it Nozzle High level (g) Intermediate Level (g) Low level (g) O_015 0.45 0.49 0.52 O_020 0.89 0.82 0.82 O_025 1.25 1.34 1.38 V21_070 0.78 0.89 0.90 V21_100 2.14 2.21 2.19 V21_145 4.20 3.46 4.37 V21_100 4.60 4.74 5.80

As already mentioned, a good linearity of the flow or a small change in mass as the tank is empty allows the user to use the same method (apply approximately the same pressure) for approximately the same time interval at any degree of filling of the tank to squeeze out approximately the same amount of liquid concentrate. Figure 18 is a graph illustrating the maximum change between two values in Table 10 for each nozzle. As shown in figure 18 and in Table 10, the maximum change for all nozzles with a round hole and with straight edges, as well as for nozzles with a cross-sectional dimensions of 0.070 and 0.100 inches, does not exceed 0.15 grams when changing the level of filling the concentrate from high to low. However, for nozzles with a cross-sectional size of 0.145 and 0.200 inches, the maximum changes were 0.91 and 1.2 grams, respectively. Most likely this is due to the variability of the opening of the hole for different pressures in combination with an increased amount of fluid flowing through the nozzle. Accordingly, an acceptable nozzle has a maximum change in flow linearity of less than 0.5 grams when the degree of filling of the container changes, preferably less than 0.3 grams and more preferably less than 0.15 grams.

As already mentioned, the design of the tank provides protection against leakage. In one embodiment, such protection is provided through the use of a cut, parts of which are flexibly bent to allow the product to pass from the container and at least partially returned to their original position to prevent unwanted fluid from flowing through the valve. Leakage protection does not mean that the tank will never leak under any conditions. The tank design provides leakage protection in the most typical conditions. The degree of leakage can be estimated using an indicator of the formation of drops. The method of determining the droplet formation rate includes providing an empty container, providing a passageway between the atmosphere and the internal volume of the container at the bottom of the container, the cross section of the passage being at least 20% of the maximum cross section of the container, filling the container with water through the passage, turning the container over, so that the outlet is directed downward, removing or opening the lid that closes the outlet, and counting water droplets that have fallen from the tank for 10 minutes. The droplet formation rate is equal to the number of droplets dropped. Tests of the preferred design of the tank having a valve with a cross-shaped cross-section V21_070 (illustrated in figure 6, but without a recess) showed that the rate of formation of drops is zero. This indicates the provision in the tank of at least substantial protection against leakage. Of course, a droplet formation index of zero is preferable, however, other suitable values include any amount in the range of 1-10 (the smaller the better).

The containers disclosed herein are suitable for a wide variety of types of liquid concentrates. Preferred are liquid concentrates suitable for cold bottling that remain usable for at least 12 months of storage at normal ambient temperature. This can be achieved by combining low pH and an alcohol content to ensure the stability of ingredients that are not in themselves stable. Compositions and corresponding methods may also include beverage concentrates having a low pH and reduced water activity, and containing alcohol. A decrease in water activity can be obtained by adding salts. Preferably, the compositions are not carbonated (e.g., using carbon dioxide). In one embodiment, the degree of dilution of the concentrate for preparing the beverage may be at least 25 times. In preferred embodiments, the concentrate may have a pH in the range of from about 1.4 to about 3.0-3.5 and alcohol in an amount of from about 3 wt.% To about 35 wt.%.

Some drinks and beverage concentrates, such as juices, are poured hot when packaging (for example, at a temperature of 93 ° C) to prevent the growth of microbes and then sealed. Other drinks, such as diet sodas, may contain preservatives and may be bottled cold during packaging (that is, without pasteurization). For the preferred compositions, taking into account the combination of their pH level and alcohol content, no additional heat or mechanical treatment, for example, pressure or ultrasonic treatment, is needed to reduce the activity of microbes, before or after packaging. Although it should be noted that for preferred compositions, such additional processing is not excluded. In preferred embodiments, the packaging material does not require additional chemical or radiation treatment. Although the production environment must be kept clean, UV treatment or the use of sterile materials is optional. In short, manufacturing equipment, the manufacturing environment and packaging should comply with the usual requirements for food production, but sterilization requirements are not imposed on packaging. Thus, the use of the above compositions can provide a reduction in production costs.

Typically, the concentrates are unsuitable for drinking and may additionally contain colorants (artificial and / or natural), flavorings (artificial and / or natural), sweeteners (artificial and / or natural), caffeine, electrolytes (including salts) and other similar additives. In some embodiments, the use of additional preservatives, such as sorbate or benzoate, to maintain the stability of the composition during storage is optional. Flavorings are stable in an acidic environment. Cold dilution is used to make drinks, and mixing with water takes place without additional stirring. The alcohol content in the finished drink should not exceed 0.5 wt.%.

To prepare a drink, the degree of dilution of the concentrate can be from 25 to 500 times. A preferred dilution range can be from about 75 to about 200 times, and more preferably from about 75 to about 160 times. The concentrate may not be drinkable until diluted and may be diluted with water. In addition to water, other liquids suitable for drinking, such as juices, carbonated drinks, tea, coffee, etc., can also be used for dilution. To clarify, a 75-fold dilution means 1 part concentrate and 74 parts water (or other liquid suitable for drinking).

When determining the preferred degree of dilution (and, accordingly, the concentration of the concentrate) for preparing the finished drink, in addition to the alcohol content, the sweetness and acidity of the drink can also be taken into account. For example, the dilution may be the degree of dilution necessary to provide a finished beverage whose sweetness level is equivalent to the sweetness of a beverage containing from about 5% to about 25% sugar. For example, the required degree of dilution can be expressed, by analogy, with an equivalent degree of brix density from 5 to 25, and preferably in the range of about 8-14. The brix density can be defined as the unit sugar content of an aqueous solution. 1 degree of brix density can correspond to 1 gram of sucrose in 100 grams of solution. For the purposes of the present embodiments, 1 degree of brix density can, by analogy, compare the amount of sweetener, natural or artificial, necessary to provide the sweetness that can be expected from an equivalent amount of sucrose. In another embodiment, dilution may be determined by preparing a finished beverage containing acidic components in the range of from about 0.01 wt.% To about 0.8 wt.%. Dilution may also be determined by preparing a finished beverage containing preservatives in an amount not exceeding about 500 ppm, preferably not more than 100 ppm.

The acidity of the concentrates may be provided by any food grade organic or inorganic acids such as citric acid, malic acid, adipic acid, tartaric acid, fumaric acid, phosphoric acid, lactic acid and the like. The pH of the concentrate can range from about 3.0 to about 1.4, preferably about 2.3, and most preferably about 2.2.

pH of the concentrate when this level is lower than necessary. For example, potassium citrate can be used to increase the pH from about 1.3 (without buffer) or 2.0 to about 2.3. See Table 11 for 3 examples. In other cases, the undissociated acid salt ion may provide buffering for the entire concentrate. In one embodiment, the pH of the concentrate provides the necessary antimicrobial effect, while the acidity is not high enough to destroy the flavor component. An additional benefit of the buffer is that it can improve the organoleptic characteristics of the final product in its diluted form. The buffer solution can improve (soften) the acidic taste of the diluted concentrate (finished drink). For example, citrate with citric acid can increase acidity better than with citric acid alone. The preferred acid / buffer ratio may be about 1: 1 or higher, preferably between 1: 1 and 40: 1, and more preferably from about 7: 1 to about 15: 1. In any case, the predetermined acid / buffer ratio contributes to the antimicrobial action and stabilization of flavor additives.

Table 11 compositions for analyzing the action of a buffer solution PH option = 1.5% PH option = 2.0% PH option = 2.5% Water 60,925 58,675 55,195 Lemon acid 24.5 24.5 24.5 Potassium sorbate 0,050 0,050 0,050 Potassium citrate 0,000 2,250 5,730 Lime juice 11.5 11.5 11.5 Sucralose 2.0 2.0 2.0 Ace one one one Dye 0,025 0,025 0,025 Total 100,0000 100,0000 100,0000

Table 12 below shows the results of the degree of change in the taste of the test samples depending on the pH level for 4 weeks. Samples of lemon concentrate liquid concentrate were prepared having pH levels of 1.5, 2.0, and 2.5, which were stored at three different temperatures: 0 ° F, 70 ° F, and 90 ° F. Samples stored at 0 ° F were control, for which it was believed that their taste did not significantly deteriorate over the indicated period. After 2 and 4 weeks, samples of liquid concentrate stored at temperatures of 0 ° F and 70 ° F were removed from their storage places and diluted with water to obtain a finished drink. Then, the resulting prepared drinks were kept until their temperature became equal to room temperature, after which they were evaluated by a group of tasters (4-6 people). Tasters first tried a sample with pH = 1.5, which was stored at 0 ° F, and compared it with a sample with pH = 1.5, which was stored at 70 ° F. Tasters then evaluated the degree of difference in taste of the samples. A rating scale of 1 to 10 was used: grades 1-3 corresponded to a slight difference, grades 4-6 corresponded to a sufficient difference, and grades 7-10 corresponded to a very large difference. The same technique was used for samples with pH levels of 2.0 and 2.5. Before tasting the following samples of tasters, they ate cookies and washed down with water. Samples stored at 90 ° F were also evaluated after 1 week, 3 weeks, 4 weeks and 5 weeks later and compared to control samples stored at 0 ° F to assess the degree of taste difference according to the procedure used for the samples. that were stored at 70 ° F. The results show that with an increase in pH, the stability of flavor additives increases.

Table 12 degree of difference in taste Concentrate stored at 70 ° F Concentrate stored at 90 ° F PH 1 Week 2 weeks 3 weeks 4 weeks pH 1 Week 2 weeks 3 weeks 4 weeks 1,5 - 4.33 - 4.00 1,5 4.00 - 6.80 6.33 2.0 - 2.00 - 3.00 2.0 2.60 - 3.20 4.67 2.5 - 2.67 - 2.00 2.5 2.20 - 4.00 4.00 Scale of difference Scale of difference Very close 1-3 Very close 1-3 Different 4-6 Different 4-6 Very different 7-10 Very different 7-10

Food antimicrobial agents used in embodiments of the invention may include various alcohols, such as ethanol, propylene glycol, or various combinations thereof. The alcohol content of the concentrate may be from about 5% to about 35%, preferably from about 5% to about 15%, and more preferably about 10% of the total weight of the concentrate. A variety of additives can be added to concentrates. As flavoring agents, fruits, tea, coffee, and the like may be used. and their combinations. The concentrate may also contain a colorant, stabilizing additives, gums, salts or nutritional supplements in any combination that maintains the desired pH and weight content of alcohol. Preferred compositions have stable aroma and color characteristics that do not change significantly in a high acid environment. Natural or artificial preservatives may be added to some compositions to maintain antimicrobial activity, such as EDTA, sodium benzoate, potassium sorbate, sodium hexametaphosphate, nisin, natamycin, polylysine, etc. Preservatives, such as potassium sorbate or sodium benzoate, may be preferred in compositions containing, for example, not more than 20 wt.% propylene glycol and / or not more than 10 wt.% ethyl alcohol. Vitamins, minerals, antioxidants, etc. can be used as nutritional supplements. In some embodiments, the concentrate contains a sweetener. Sweeteners suitable for the purposes of the present invention include sucralose, aspartame, saccharin, monatin, luo han guo, neotam, sucrose, fructose, cyclamates, potassium acelsulfam or any other high-calorie or non-nutritive sweeteners and combinations thereof. The following Tables provide specific variations of the various concentrate compositions.

Table 13 cold bottled beverage concentrate (first example) Set value Range Ingredients Weight,% Min Max. Water 47.00 30.00 65.00 Lemon acid 20.00 15.00 40.00 Potassium citrate 0.75 0.00 4.00 Flavoring 17.45 10.00 30.00 Sucralose 1.00 0.50 4.00 Ace 0.75 0.10 2.00 Ethanol 13.00 5.00 30.00 Dyes 0.05 0.005 5 Total: 100.00

Table 14 cold bottled beverage concentrate (second example Set value Range Ingredients Weight,% Min Max. Water 49.00 30.00 65.00

Lemon acid 16.00 5.00 35.00 Apple acid 5.00 1.00 30.00 Potassium citrate 0.71 0.00 4.00 Flavoring 15,99 10.00 30.00 Sucralose (dry) 1,50 0.50 4.00 Ace 0.50 0.10 2.00 Ethanol 11.00 5.00 30.00 Dyes 0.30 0,03 5 Total: 100.00

Table 15 cold bottled beverage concentrate (third example) Preset value (few electrolytes) Preset value (many electrolytes) Range Ingredients Weight,% Weight,% Min Max. Water 55.41 42.17 20.00 70.00 Lemon acid 17.9 17.9 5.00 30.00 Potassium sorbate 0.05 0.05 0.00 0.10 Potassium citrate 1,5 2.9 0.00 5.00 Dye / alcohol 12,2 12,2 1.00 40.00 Sucralose 2.01 2.01 0.00 20.00 Apple acid 4,5 4,5 0.00 30.00 Ace 0.99 0.99 0.00 5.00 Dye 0.17 0.20 0.00 2.00 Potassium monophosphate 1.19 4.13 0.00 10.00 Salt (NaCl) 4.08 12.95 0.00 20.00 In total (without water): 44.59 57.83 Total: one hundred one hundred Range Few A lot of Water activity in concentrate: 0.93 0.78 0.6 up to 1.0 8 oz Sodium (mg) 35.00 111.00 1.00 200.00

8 oz potassium of the drink (mg) 20.00 50.00 1.00 100.00

Table 16 cold bottled beverage concentrate (fourth example) Set value Ingredients Weight,% Water 67.07 Lemon acid 11.8 Potassium sorbate 0.05 Potassium citrate 1,08 Dye / alcohol 8.2 Sucralose (liquid) 4.9 Apple acid 3.0 Ace 0.6 Potassium monophosphate 0.4 NaCl 2.9 Total: one hundred Valid. pH 1.88 Valid. density 1.09

Table 17 cold bottled beverage concentrate (fifth example) Set value Ingredients Weight,% Water 61.03 Lemon acid 11.2 Potassium sorbate 0.05 Potassium citrate 1,02 Dye / alcohol 7.8 Sucralose (liquid) 4.7 Apple acid 2,8 Ace 0.6

Potassium monophosphate 2.0 NaCl 8.8 Total: one hundred Valid. pH 1.78 Valid. density 1.16

The examples presented in Tables 13-17 include compositions for cold bottling beverage concentrates with a low pH, not exceeding about 3.5 and preferably in the range from about 1.7 to about 2.4. Ethanol, propylene glycol and the like can be used as alcohol. and their combinations. The alcohol content may be in the range from about 1 wt.% To about 35 wt.% And preferably in the range from about 3 wt.% To about 35 wt.%. Alcohol is included in the above examples of compositions along with flavoring. However, the total weight content of alcohol should be in the indicated ranges, regardless of their combination with dyes. In addition, in the examples given in Tables 13 to 17, various combinations of salts are indicated, the content of which is in the range of up to about 35 wt.% And preferably in the range of from about 4 wt.% To about 15 wt.%. Dyes can be artificial or natural, and their content can be in the range from 0.005% to 5.0%, preferably in the range from about 0.005% to about 1%. In compositions that use natural dyes, their higher content may be required to obtain the desired color characteristics.

As shown in Tables 13-17, in addition to potassium citrate, the compositions also contain components that reduce the activity of water in the compositions, for example, salts such as sodium chlorine (NaCl) and potassium monophosphate. These added salts may reduce the activity of the concentrate water to increase the stability of antimicrobial properties. Compositions labeled “Low Electrolytes” contain little NaCl and potassium monophosphate, and compositions labeled “Many Electrolytes” have a higher content of NaCl and potassium monophosphate. Although it should be noted that in the above examples, it is possible to use a higher and lower salt content. The added salts can provide a beverage liquid concentrate composition that can be diluted at least 75 times and preferably up to a ratio of 100 times, and the water activity in such a composition can be in the range of about 0.6 to about 1 (preferably in the range of about 0.75 to about 1).

(кальций);

(магний); Cl^- (хлорид);

(кислый фосфат);

(гидрокарбонат) и им подобные вещества и их сочетания. Другие добавляемые соли могут включать электролиты, такие как, например: лимоннокислый натрий; монофосфат натрия; хлористый натрий; хлористый калий; хлористый магний; хлористый кальций и им подобные вещества и их сочетания. Как известно эти соли обеспечивают электролиты, которые используются в напитках для спортсменов. Предполагается, что эти композиции концентратов напитков с содержанием компонентов в указанных диапазонах могут иметь достаточные противомикробные свойства без использования консервирующих добавок, и стабильность компонентов будет обеспечиваться по меньшей мере в течение года при хранении при обычных температурах.With a decrease in water activity, the shelf life of the product is increased and the antimicrobial properties are improved, which reduces the alcohol content and preservative additives. Water activity can be defined as the ratio of water vapor pressure in a sealed chamber containing a food product to the pressure of saturated water vapor at the same temperature. Thus, the activity of water may indicate the extent to which unbound water may act as a solvent or otherwise impair the properties of the product or contribute to the development of microbiological reactions. See, for example, US Pat. No. 6,482,465 by Cherukuri et al. Salts containing Na ⁺ (sodium) may be used in concentrates; K ⁺ (potassium);

(calcium);

(magnesium); Cl ^- (chloride);

(acid phosphate);

(bicarbonate) and the like, and combinations thereof. Other added salts may include electrolytes, such as, for example: sodium citrate; sodium monophosphate; sodium chloride; potassium chloride; magnesium chloride; calcium chloride and the like, and combinations thereof. As you know, these salts provide electrolytes that are used in drinks for athletes. It is contemplated that these beverage concentrate compositions containing components in the indicated ranges may have sufficient antimicrobial properties without the use of preservative additives, and the stability of the components will be ensured for at least a year during storage at ordinary temperatures.

To study the antimicrobial properties of the considered beverage concentrate compositions of the present invention, studies were conducted using different pH and alcohol levels to identify combinations that adversely affect microbial reproduction or have no effect at all. As a rule, at a high pH level (namely, 3 and above) and a low alcohol content (namely, below about 5 wt.%), Some mold development was observed. Compositions for which there was a negative effect on the reproduction of microbes, or the antimicrobial effect was zero, were also tested to assess their organoleptic characteristics.

In particular, Tables 18 and 19 present the results of determining the antimicrobial properties for several variants of potential beverage concentrates depending on the pH level and alcohol content (Table 18 for EtOH and Table 19 for propylene glycol). The antimicrobial properties of EtOH were determined for three types of crops: microbes , yeast and mold, and tests were carried out for at least 3 months. The following microbial cultures were used in the trials: Gluconobacter oxydans, Gluconacetobacter diazotrophicus, Gluconacetobacter liquefaciens, and / or Gluconobacter sacchari. Yeast cultures contained Zygosaccharomyces bailii, Saccharomyces cerevisiae, Candida tropicalis and / or Candida lypolytica. Mold cultures contained Penicillium spinulosum, Aspergillus niger and / or Paecilomyces variotii. The results show that the impact on which crops was negative, or it was zero, compared with the control samples, the indication * corresponds to the absence of reproduction of microbes, and *** corresponds to some reproduction. Tests using mold and yeast were also performed for samples in which propylene glycol was used as alcohol. For these samples, the pH was about 2.3, the activity of water ranged from about 0.85 to about 0.95. Table 19 shows a positive relationship between increased levels of propylene glycol and improved antimicrobial activity.

Table 18 antimicrobial properties Option pH EtOH,% Germs Yeast Mold All one 3.0 fifteen * * * * 2 3.0 10 * * * * 3 3.0 5 * *** *** *** four 2.5 fifteen * * * * 5 2.5 10 * * * * 6 2.5 5 * * * * 7 2.0 fifteen * * * * 8 2.0 10 * * * * 9 2.0 5 * * * * 10 1,5 fifteen * * * * eleven 1,5 10 * * * * 12 1,5 5 * * * *

C1 3.0 0 * *** *** *** C2 1,5 twenty * * * * C3 1,5 0 * * *** *** C4 3.0 twenty * * * *

Table 19 antimicrobial properties Results for mold Propylene Glycol Week 4 0% one hundred 10% 1200 fifteen% 300 twenty% <1 25% <1 Results for Yeast Propylene Glycol Week 4 0% <100 10% <100 fifteen% <100 twenty% <100 25% <10

Tests for microbes gave a similar low or zero antimicrobial effect. A decrease in the activity of water in the compositions of salts was also investigated. In particular, the activity of water in a composition containing water in an amount of about 68 wt.%, Citric acid is about 2 wt.%, Potassium citrate is about 1.5 wt.%, Flavor / alcohol is about 8.5 wt.%, sucralose — about 1.9 wt.%, malic acid — about 17 wt.% and AceK — about 1.1 wt.%, was about 0.94. When 7 wt.% And 13 wt.% Water was replaced with a salt (NaCl), the water activity dropped to about 0.874 and 0.809, respectively. Unexpectedly, it turned out that such levels of water activity (for example, about 0.8) in combination with a low pH and alcohol content provided the antimicrobial effect that was provided by the previous compositions with water activity not exceeding about 0.6. See Table 20. Thus, the combination of a low pH, an alcohol (for example, propylene glycol, ethanol and the like alcohols and their combinations) and a reduced activity of water create an environment unfavorable for microorganisms. Such a combination of pH and water activity in preferred embodiments can have an antimicrobial effect with an ethanol content of about 10% and a propylene glycol of about 20% and a bacteriostatic effect with a propylene glycol content of about 10%.

Table 20 antimicrobial compositions Ingredients Composition 1 Composition 2 Composition 3 Water activity - 0.940% Water activity - 0.874% Water activity - 0.809% Water 68 61 55 Lemon acid 2 2 2 Salt (NaCl) 0 7 13 Potassium citrate 1,5 1,5 1,5 Dye / alcohol 8.5 8.5 8.5 Sucralose (dry) 1.9 1.9 1.9 Apple acid 17 17 17 Ace 1,1 1,1 1,1 Total one hundred one hundred one hundred

The implementation of the present invention may include any number of changes to obtain a beverage concentrate with a desired pH and alcohol content. In general, the method may include providing water and additives, followed by providing alcohol in an amount of at least 5 wt.% And an acid component for controlling the change in pH so that it does not exceed at least about 3. Buffer solutions may also be added.

Other examples of suitable liquid concentrates are shown in Table 21 below. These concentrates can be used in conjunction with the above containers to provide packages with beverage concentrates that have a longer shelf life. These concentrates can also be used independently of the containers disclosed in this application, that is, separately or with other types of containers. It should be noted that the flavoring portion of the composition, as indicated in Table 21, includes the combined flavoring / alcohol component. The alcohol content in the composition in wt.% Is indicated in parentheses. Ethyl alcohol, propylene glycol and combinations thereof can be used as alcohol, and alcohol is used as a solvent for flavoring. The alcohol content may be from about 75% to about 95% of the flavoring portion of the composition, and is preferably about 90%.

Table 21 beverage concentrate examples Compositions: one 2 3 four 5 6 7 8 Ingredients (wt.%) % % % % % % % % Water 60-65 52-58 60-65 60-65 60-65 70-75 55-60 58-63 Lemon acid 1-4 15-20 1-4 5-9 1-4 0-1 15-20 15-20 Potassium citrate 1-3 1-3 1-3 1-3 1-3 0-1 1-3 1-3 Sucralose, 25% 5-10 5-10 5-10 5-10 5-10 5-10 5-10 5-10 Apple acid 15-20 3-5 15-20 10-14 13-17 2-6 0-2 0-2 Acesulfame K 0.5-1.5 0.5-1.5 0.5-1.5 0.5-1.5 0.5-1.5 0.5-1.5 0.5-1.5 0.5-1.5 Potassium sorbate 0.01-0.1 0.01-0.1 0.01-0.1 0.01-0.1 0.01-0.1 0.01-0.1 0.01-0.1 0.01-0.1 Fragrance (alcohol) 7-12 (6-11) 10-14 (9-13) 7-12 (6-11) 7-12 (6-11) 10-14 (9-13) 12-16 (11-14) 10.5-16 (9-14) 6-10 (5-9) A mixture of caffeine with taurine 2-4 2-4 Trisodium Citrate 1-3 1-3 Dye 0.05-0.2 0.051-0.21 0.065-0.28 0.1-0.9 0.021-0.104 0.201-1.004 0,101-0,504 0,101-0,509

The combined use of the nozzle 132 and the closing part 126 with the clogging part 148 and the inner plug 149, as shown in figures 19 and 20, provide several levels of protection against leakage, which is especially important when used with the beverage concentrates disclosed in this application. This very high degree of protection becomes apparent when compared with a screw cap, which is used, for example, in a bottle with Visine, but a hinged lid is easier to use than a screw cap. As indicated in Table 22, when the V21_070 nozzle is used, the amount of oxygen that enters the closed container over time is comparable to the amount of oxygen for the screw cap of the Visine bottle.

Table 22 clogging characteristics (by the amount of incoming oxygen) Day one 2 four 10:30 11:15 12:00 10 a.m. 4:00 10:30 Variable Sample, # O ₂ % O ₂ % O ₂ % O ₂ % O ₂ % O ₂ % Capacity with V21_070 one 0.14 0.15 0.19 2.04 2.15 2.87 2 0.02 0.11 0.18 3.21 3.4 4.61 3 0.04 0,07 0.09 1.12 1,2 1.65 Visine one 0.05 0.09 0.13 2,56 2.77 4.1 2 0.15 0.16 0.18 2.25 2.43 3,58

The drawings and the above description should not be construed as the only forms of capacity and methods in relation to structural details. You must understand that, depending on the situation, various changes in the shape and ratio of parts, as well as their replacement with equivalents, can be proposed. Similarly, while beverage concentrates and methods have been discussed in the present description with specific embodiments of the invention, it should be understood that various alternatives, modifications, and variations of the options discussed in the description will be apparent to those skilled in the art upon review of the description.

Claims (36)

1. A packaged product in a container having multiple doses of a liquid beverage concentrate, the container comprising a body having a closed lower end, an upper end with an outlet, and a side wall extending between the upper and lower ends, which form an internal volume of the container body with access through an outlet of the upper end, while the side wall is configured to be pressed onto it to expel the liquid beverage concentrate from the internal volume of the container body and then through the outlet; and an exhaust outlet path including an nozzle for dispensing a liquid beverage concentrate in a jet when a side wall is squeezed having an average mass flow rate for pressure forces of about 100 inches v. and about 40 inches east, comprising from about 16.5 g / s to about 0.4 g / s. 2. The packaged product of claim 1, wherein the average mass flow rate is from about 16.5 g / s to about 2.1 g / s. 3. The packaged product according to claim 2, in which the functional indicator of the dosed delivery of liquid concentrate (LCDFV) is in the range from 1 to 4. 4. The packaged product according to claim 1, in which the exhaust path is arranged in such a way that the value of the index of the ability to mix a jet of liquid concentrate exiting the tank does not exceed 2. 5. The packaged product according to claim 1, in which the exhaust path is arranged in such a way that the magnitude of the impact spatter of the jet of liquid concentrate does not exceed 3. 6. The packaged product of claim 1, further comprising a lid attached to the container body and having a closure portion for selectively closing the outlet and locking the outlet.       7. The packaged product according to claim 6, in which the lid has a base with an outer skirt forming a smooth transition to the side wall of the container body below the protrusion, and the cover part of the lid has an outer part forming a smooth transition to the outer skirt of the base of the lid when the cover part of the lid put on the base of the cover. 8. The packaged product according to claim 6, in which the movement of the closing part of the lid in the closed position, blocking the flow, is accompanied by at least two triggering signals - audible and tactile. 9. The packaged product according to claim 6, also comprising means for generating an audible and / or tactile response signal when moving the closing part of the lid to the closed position, blocking the flow. 10. The packaged product according to claim 6, in which the closing part of the lid includes means for blocking the exhaust path. 11. The packaged product of claim 1, also having a droplet index of zero. 12. The packaged product according to claim 1, in which the nozzle located in the exhaust tract is adapted to form a jet of liquid concentrate having an indicator of the performance of the liquid concentrate not exceeding 6 when a force is applied to the side wall that creates a speed from about 2400 to 4400 mm / s 13. The packaged product according to claim 12, in which the nozzle is a valve containing several slots forming several valves that can move between the clogged position, when there is essentially no force applied to the side wall, and the bent position, in which through them pass the liquid concentrate when a force is applied to the side wall. 14. The packaged product according to p. 12, in which the nozzle design provides a maximum difference in the time of extrusion of a jet of 4 cm ^{3 of} liquid concentrate ejected from the tank, for strong pressure, providing a speed of from about 5600 to 7600 mm / s compared to weak pressure, providing speed from about 2400 to 4400 mm / s, component of less than about 2 seconds. 15. The packaged product of claim 12, further comprising a closable lid that attaches to the upper end of the container body and further forms an outlet path such that pressure pushing the liquid concentrate from the inner volume of the vessel body pushes the liquid concentrate through the nozzle of the outlet path; and means for generating an audible and / or tactile response signal when the lid is closed. 16. The packaged product according to any one of paragraphs. 1-15, in which the concentrate contains at least about 5 wt.% Alcohol and from 1% to 40% flavoring and has a pH of less than about 3.5, and the pH is adjusted using acid and buffer at an acid / a buffer ranging from about 1: 1 to about 4000: 1. 17. The packaged product of claim 16, wherein the viscosity of the concentrate is less than about 500 cP. 18. The packaged product of claim 16, wherein the viscosity of the concentrate is in the range of about 1 cP to about 25 cP. 19. The packaged product of claim 16, wherein the alcohol is propylene glycol. 20. The packaged product of claim 16, wherein the acid / buffer weight ratio is in the range of from about 1: 1 to about 40: 1. 21. The packaged product according to claim 16, in which the concentration of the concentrate is in the range from about 25 times to about 500 times. 22. The packaged product of claim 16, wherein the pH is in the range of about 1.4 to about 3.0. 23. The packaged product of claim 16, wherein the pH is adjusted using a food acid selected from the list consisting of citric acid, malic acid, fumaric acid, tartaric acid, phosphoric acid, and lactic acid. 24. The packaged product of claim 16, wherein the pH is in the range of about 1.7 to about 2.4. 25. A method of obtaining a mixture using a jet of liquid concentrate from a container, including: creating a pressure difference between the external environment and the internal volume of the tank, sufficient to push the liquid concentrate from the tank containing many doses stored inside the liquid concentrate, and an outlet with a nozzle; dosed delivery of a stream of liquid concentrate from a container at a height of about 2 to about 4 inches above a given vessel, through a nozzle with a container oriented at an angle of about 0 to about 10 degrees relative to the vertical, while the stream of liquid concentrate has an average mass flow for pressure forces about 100 inches and about 40 inches in. Art., comprising from about 16.5 g / s to about 0.4 g / s; the action of a jet on a given liquid inside a given vessel so that when exposed to a specified vessel, a noticeable amount of fluid is not forced out; mixing a given liquid and liquid concentrate with a stream to obtain a generally homogeneous mixture. 26. The method according to p. 25, in which when the jet is applied to a given liquid inside a given vessel, the impact spatter is less than 3. 27. The method according to p. 25, in which the mixing of a given liquid and liquid concentrate with a stream includes mixing to obtain a generally homogeneous mixture having a pH difference between the lower and upper parts of a given vessel equal to 0.3, 10 seconds after exposure to a given liquid. 28. The method according to p. 25, in which the mixing of a given liquid and liquid concentrate stream provides a measure of the ability of mixing less than 3. 29. The method according to p. 25, in which a metered discharge from the tank through the nozzle of the jet of liquid concentrate provides a mass flow rate of 1.0 g / s to 5 g / s, and the issuance of a portion of the liquid concentrate is carried out over a time interval in the range from 0.3 to 3.0 seconds. 30. The method according to p. 25, in which when dosed discharge from the tank through the nozzle of the jet of liquid concentrate provides a mass flow rate from 1.0 g / s to 5 g / s, more preferably from 1.0 g / s to 1.5 g / sec

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